Methods and compositions for treating subterranean formations with gelled hydrocarbon fluids

ABSTRACT

Improved methods and compositions for treating subterranean formations penetrated by well bores are provided. A method for breaking a gelled hydrocarbon fluid comprised of a hydrocarbon liquid, a ferric iron or aluminum polyvalent metal salt of a phosphonic acid ester or dialkylphosphinic acid is provided.

CROSS REFERENCE TO RELATED APPLICATION

[0001] This application is a continuation-in-part of U.S. patentapplication Ser. No. 09/792,165 filed Feb. 23, 2001, entitled “Methodsand Compositions for Treating Subterranean Formations with GelledHydrocarbon Fluids, now U.S. Pat. No. 6,544,934.

Background of the Invention

[0002] 1. Field of the Invention

[0003] This invention relates to gelled liquid hydrocarbon fluids andmethods of their use and preparation.

[0004] 2. Description of the Prior Art

[0005] High viscosity gelled hydrocarbon liquids have heretofore beenutilized in treating subterranean formations penetrated by well bores,e.g., hydraulic fracturing stimulation treatments. In such treatments, ahigh viscosity gelled liquid hydrocarbon fracturing fluid havingparticulate proppant material, e.g., sand, suspended therein is pumpedthrough a well bore into a subterranean formation to be stimulated at arate and pressure such that one or more fractures are formed andextended in the formation. The suspended proppant material is depositedin the fractures when the gelled hydrocarbon fracturing fluid is brokenand returned to the surface. The proppant material functions to preventthe formed fractures from closing whereby conductive channels remainthrough which produced fluids can readily flow to the well bore.

[0006] Polyvalent metal salts of orthophosphoric acid esters haveheretofore been utilized as gelling agents for forming high viscositygelled liquid hydrocarbon fracturing fluids. Such gelled liquidhydrocarbon fracturing fluids have included fracture proppant materialand delayed breakers for causing the fracturing fluids to break intorelatively thin fluids whereby the proppant material is deposited informed fractures and the fracturing fluid is produced back. Descriptionsof such heretofore utilized high viscosity gelled liquid hydrocarbonfracturing fluids and methods of their use are set forth in U.S. Pat.No. 4,622,155 issued to Harris et al. on Nov. 11, 1986, and U.S. Pat.No. 5,846,915 issued to Smith et al. on Dec. 8, 1998. The gelled liquidhydrocarbon fracturing fluids described in the above patents utilizeferric iron or aluminum polyvalent metal salts of phosphoric acid estersas gelling agents and delayed breakers such as hard burned magnesiumoxide which is slowly soluble in water.

[0007] While the heretofore utilized high viscosity gelled liquidhydrocarbon fracturing fluids and methods have been used successfullyfor forming fractures in subterranean formations, problems have beenencountered as a result of the use of the gelling agent, i.e., thepolyvalent metal salt of a phosphoric acid ester. That is, in recentyears plugging of refinery towers which process oil produced fromformations fractured with gelled liquid hydrocarbon fracturing fluidshas caused many expensive, unplanned shut-downs. The plugging materialis high in phosphorus and has been attributed to the phosphate estersused as gelling agents. The phosphate esters contribute volatilephosphorus which condenses on distillation tower trays, causingplugging. The volatile phosphorus may also carry over the tops of thedistillation towers causing contamination of the hydrocarbon productsproduced.

[0008] Thus, there are needs for improved methods of using and preparinggelled liquid hydrocarbons which upon breaking and being refinedsubstantially reduce volatile phosphorus in distillation towers,improved liquid hydrocarbon gelling agents and improved gelled liquidhydrocarbon compositions. More specifically, in fracturing oil producingsubterranean formations in areas where volatile phosphorus is a problemin refineries, there is a need to reduce the production of volatilephosphorus in the refineries to levels where the above describedunscheduled refinery shut downs are not required without compromisingCO₂ compatibility with the gelled oil fracturing fluids used.Concentrations of CO₂ as high as 40-50% are commonly used in gelled oilfracturing fluids which form miscible mixtures with the fluids. Thepresence of the CO₂ enhances fluid recovery, minimizes the amount of oilbased fracturing fluid which must be recovered, and reduces costs inareas where CO₂ is less expensive than the oil based fracturing fluid.

SUMMARY OF THE INVENTION

[0009] The present invention provides improved methods of using andpreparing gelled liquid hydrocarbons, improved liquid hydrocarbongelling agents and improved gelled liquid hydrocarbon compositions whichmeet the above described needs and overcome the deficiencies of theprior art.

[0010] The improved methods of this invention for fracturingsubterranean formations using gelled liquid hydrocarbons are basicallycomprised of the following steps. An improved gelled liquid hydrocarbonfracturing fluid is prepared comprised of a hydrocarbon liquid, agelling agent comprised of a ferric iron or aluminum polyvalent metalsalt of a phosphonic acid ester or a dialkylphosphinic acid, a proppantmaterial, water and an amount of a delayed gel breaker effective tobreak the gelled hydrocarbon fracturing fluid. The phosphonic acid esterutilized in the gelling agent which minimizes volatile phosphorus inrefinery distillation towers has the formula:

[0011] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms. The dialkylphosphinic acid utilized in the gelling agenthas the formula:

[0012] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms. After the gelled liquidhydrocarbon fracturing fluid is prepared, the subterranean formation tobe fractured is contacted with the gelled liquid hydrocarbon fracturingfluid under conditions effective to create at least one fracture in thesubterranean formation.

[0013] The improved methods of this invention for preparing gelledliquid hydrocarbons basically comprise adding a phosphonic acid esterhaving the formula:

[0014] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms, or a dialkylphosphinic acid having the formula:

[0015] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms and preferably, at least astoichiometric amount of a polyvalent metal source selected from ferriciron salts and aluminum compounds to a hydrocarbon liquid. Thepolyvalent metal source reacts with the phosphonic acid ester ordialkylphosphinic acid to form a ferric iron or aluminum polyvalentmetal salt thereof. Water and an amount of a delayed gel breakereffective to break the gelled liquid hydrocarbon fracturing fluid mayalso added to the hydrocarbon liquid.

[0016] The improved liquid hydrocarbon gelling agents of this inventionare comprised of a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester or a dialkylphosphinic acid, the phosphonic acidester having the formula:

[0017] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms and the dialkylphosphinic acid having the formula:

[0018] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms.

[0019] The improved gelled liquid hydrocarbon compositions of thisinvention are comprised of a hydrocarbon liquid, a gelling agentcomprising a polyvalent metal salt of a phosphonic acid ester ordialkylphosphinic acid and a ferric iron salt or an aluminum compound,the phosphonic acid ester having the formula:

[0020] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms, and the dialkylphosphinic acid having the formula:

[0021] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms.

[0022] Other features and advantages of the present invention will bereadily apparent to those skilled in the art upon a reading of thedescription of preferred embodiments which follows.

DESCRIPTION OF PREFERRED EMBODIMENTS

[0023] The present invention provides methods of treating subterraneanformations penetrated by well bores with gelled liquid hydrocarbonfluids. For example, the gelled liquid hydrocarbon fluids are suitablefor use in fracturing treatments carried out in subterranean formationswhereby the production of hydrocarbons from the subterranean formationsis stimulated. In accordance with the present invention, a fracturingfluid comprised of a gelled liquid hydrocarbon or mixture ofhydrocarbons containing a proppant material and a delayed gel breaker ispumped through a well bore into a subterranean formation to bestimulated. The fracturing fluid is pumped at a rate and pressure suchthat one or more fractures are formed and extended in the subterraneanformation. The proppant material which is suspended in the fracturingfluid is deposited in the fractures when the gel is broken and returnedto the surface. The proppant material remains in the fractures andfunctions to prevent the fractures from closing whereby conductivechannels are formed through which produced fluids can readily flow fromthe subterranean formation into the well bore.

[0024] As mentioned above, gelled liquid hydrocarbon fracturing fluidshave heretofore been formed with a gelling agent comprised of a ferriciron or aluminum polyvalent metal salt of a phosphoric acid ester. Thephosphoric acid ester suffers from the problem that it decomposes inrefinery distillation towers to form volatile phosphorus which condenseson the trays of the distillation towers and causes plugging. Also, thephosphoric acid ester may itself be volatile, dependent upon itsmolecular weight. By the present invention, improved methods andcompositions for fracturing subterranean formations with gelled liquidhydrocarbon fracturing fluids are provided wherein the gelling agentutilized is a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester or dialkylphosphinic acid. Unlike the phosphoricacid esters utilized heretofore, the phosphonic acid esters ordialkylphosphinic acids of the present invention have much higherthermal stability and the dialkylphosphinic acids have higher hydrolyticstability and consequently do not as readily decompose or disassociate.

[0025] Thus, the improved methods of fracturing subterranean formationsof the present invention are basically comprised of the following steps.A gelled liquid hydrocarbon fracturing fluid is prepared comprised of ahydrocarbon liquid, a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester or a dialkylphosphinic acid, a proppant material,water and an amount of a delayed gel breaker effective to break thegelled liquid hydrocarbon fracturing fluid. The phosphonic acid esterhas the formula:

[0026] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms. The dialkylphosphinic acid has the formula:

[0027] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms. After the gelled liquidhydrocarbon fracturing fluid is prepared, the subterranean formation tobe fractured is contacted with the fracturing fluid under conditionseffective to create at least one fracture in the subterranean formation.

[0028] The hydrocarbon liquid utilized to form the gelled liquidhydrocarbon fracturing fluid can be any of the various previously usedhydrocarbon liquids including, but not limited to, olefins, kerosene,diesel oil, gas oil (also known as gas condensate), fuel oil, otherpetroleum distillates, and certain mixtures of crude oil. Liquidhydrocarbon fracturing fluids which are specifically designed for usewith CO₂ are generally preferred. Such a liquid hydrocarbon fracturingfluid is commercially available from the Trysol Corporation of Sundre,Alberta, Canada under the trade name “FRACSOL™.”

[0029] As mentioned above, the gelling agent utilized for gelling thehydrocarbon liquid whereby it has a high viscosity sufficient to carrysuspended proppant material and produce fractures in a subterraneanformation is a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester or dialkylphosphinic acid having the formula setforth above. The polyvalent metal salt of the phosphonic acid ester ordialkylphosphinic acid is preferably produced at the well site by addingthe phosphonic acid ester or dialkylphosphinic acid, and preferably, atleast a stoichiometric amount of a polyvalent metal salt (preferably aferric iron salt or an aluminum compound). In addition, in a preferredembodiment, if water is not already contained in the hydrocarbon liquidor added thereto as a component in a cross-linker solution or the like,water is added to the hydrocarbon liquid in an amount, for example, ofabout 0.05% or greater by weight of the hydrocarbon liquid. The presenceof the water allows slowly water soluble or encapsulated breakers to bedissolved or released. See, for example, Smith et al. U.S. Pat. No.5,846,915 issued on Dec. 8, 1995 which is incorporated herein byreference.

[0030] When a ferric iron salt is utilized to form the gelling agent, itis preferably selected from ferric sulfate or ferric chloride withferric sulfate being preferred. The ferric iron salt is typically mixedwith amines, surfactants and water to form a liquid cross-linkingsolution. An example of a commercially available ferric ironcross-linking solution is “EA-3™” cross-linking solution sold by EthoxChemicals, Inc. of Greenville, South Carolina. When an aluminum compoundis utilized, it is preferably selected from aluminum chloride oraluminum isopropoxide, with aluminum chloride being the most preferred.The polyvalent metal compound utilized reacts with the phosphonic acidester or dialkylphosphinic acid to form the hydrocarbon liquid gellingagent of this invention which gels the hydrocarbon liquid. Thephosphonic acid ester or dialkylphosphinic acid is added to thehydrocarbon liquid along with the polyvalent metal source to form thegelling agent in the hydrocarbon liquid in an amount in the range offrom about 0. 1% to about 2.5% by weight of the hydrocarbon liquid.

[0031] As mentioned above, the phosphonic acid ester which can beutilized to form the hydrocarbon liquid gelling agent of this inventionhas the formula:

[0032] wherein R is an alkyl group having from about 6 to about 24carbon atoms and R′ is an alkyl group having from about 1 to about 4carbon atoms. Techniques which can be utilized for the preparation ofthe phosphonic acid esters useful in accordance with this invention are,for example, described in U.S. Pat. No. 3,798,162 issued to Dickert, Jr.on Mar. 19, 1974 which is incorporated herein by reference.

[0033] The dialkylphosphinic acid which can be utilized to form thehydrocarbon liquid gelling agent of this invention has the formula:

[0034] wherein R¹ is methyl, ethyl, n-propyl, i-propyl, n-butyl orsec-butyl and R² is a straight chain or branched alkyl or phenyl grouphaving from about 6 to about 24 carbon atoms. Techniques which can beused for the preparation of the dialkylphosphinic acid useful inaccordance with this invention are well known. For example, thedialkylphosphinic acid can be prepared from the reaction ofalkylphosphonic dichloride with a Grignard reagent as reported by Croftsand Fox in “Unsymmetrical dialkylphosphinic acids” J. Chem. Soc. 1958,2995-2997 the entire disclosure of which is incorporated by reference.The reaction sequence is illustrated below:

[0035] Alternatively, the unsymmetrical dialkyphosphinic acids can beprepared in a one-pot synthesis using the method of Boyd et al in“Synthesis of γ-keto-substituted phosphinic acids frombis(trimethylsilyl)phosphonite and α,β-unsaturated ketones,” TetrahedronLett., 1992, 33, 813-816 and Boyd, E. A.; Regan, A. C.; James, K.“Synthesis of alkyl phosphinic acids from silyl phosphonites and alkylhalides,” Tetrahedron Lett., 1994, 35, 4223-4226, the entire disclosuresof which are incorporated herein by reference. The reaction sequence isillustrated below:

[0036] Proppant materials which can be utilized in the fracturing fluidsof this invention are well known in the art. For example, proppantmaterials such as graded walnut or other nut shells, resin coated walnutor other nut shells, graded sand, resin coated sand, sintered bauxite,various particulate ceramic materials, glass beads and the like can beutilized. The particular size of the proppant material employed dependson the particular formation being fractured and other variables.Generally, the proppant particle sizes are in the range of from about 2to about 200 mesh on the U.S. Sieve Series scale.

[0037] A variety of delayed gel breakers can be utilized in accordancewith the present invention to cause the gelled liquid hydrocarbonfracturing fluid to revert to a thin fluid that is produced back afterfractures are formed in a subterranean formation. The gel breakers canbe materials which are slowly soluble in water which, as mentionedabove, may be combined with or otherwise present in the hydrocarbonliquid. The breaking of the gel does not take place until the slowlysoluble breakers are dissolved in the water. Examples of such slowlysoluble breakers are given in U.S. Pat. No. 5,846,915 issued to Smith etal. on Dec. 8, 1998 which is incorporated herein by reference. Asindicated in U.S. Pat. No. 5,846,915, hard burned magnesium oxide havinga particle size which will pass through a 200 mesh Tyler screen ispreferred. The hard burned magnesium oxide and other similar breakersare not immediately present for breaking the gel due to their slowlysoluble nature. Other breakers such as alkali metal carbonates, alkalimetal bicarbonates, alkali metal acetates, other alkaline earth metaloxides, alkali metal hydroxides, amines, weak acids and the like can beencapsulated with slowly water soluble or other similar encapsulatingmaterials. Such materials are well known to those skilled in the art andfunction to delay the breaking of the gelled hydrocarbon liquid for arequired period of time. Examples of water soluble and other similarencapsulating materials which can be utilized include, but are notlimited to, porous solid materials such as precipitated silica,elastomers, polyvinylidene chloride (PVDC), nylon, waxes, polyurethanes,cross-linked partially hydrolyzed acrylics and the like. Of the slowlysoluble or encapsulated breakers mentioned, hard burned magnesium oxidewhich is commercially available from Clearwater Inc. of Pittsburgh, Pa.is preferred for use in accordance with the present invention. When analkaline breaker is utilized, e.g., magnesium oxide, the acid group ofthe phosphonic acid ester in the gelling agent is neutralized whichinitially increases the viscosity of the gelled hydrocarbon liquid afterwhich the gel is broken. The alkaline breaker will also neutralize thedialkylphosphinic acid in the gelling agent.

[0038] Another type of breaker which can be utilized when the gellingagent is a ferric iron polyvalent metal salt of a phosphonic acid esterof this invention, or a ferric iron polyvalent metal salt of thedialkylphosphinic acid, is a reducing agent that reduces ferric iron toferrous iron. Of the various oxidation states of iron, only ferric ironis capable of forming a viscous coordination complex with a phosphonicacid ester or dialkylphosphinic acid, therefore the complex can bedisassociated by reducing the ferric iron to the ferrous state. Thedisassociation causes the gelled hydrocarbon liquid to break. Examplesof reducing agents which can be utilized include, but are not limitedto, stannous chloride, thioglycolic acid (2-mercaptoacetic acid),hydrazine sulfate, sodium diethyldithiocarbamate, sodiumdimethyldithiocarbamate, sodium hypophosphite, potassium iodide,hydroxylamine hydrochloride, thioglycol (2-mercaptoethanol), ascorbicacid, sodium thiosulfate, sodium dithionite and sodium sulfite. Ofthese, the preferred reducing agents for use at a temperature of about90° C. are stannous chloride, thioglycolic acid, hydrazine sulfate,sodium diethyldithiocarbamate and sodium dimethyldithiocarbamate. Themost preferred reducing agent is thioglycolic acid which may be delayedby salt formation or encapsulation. As mentioned above in connectionwith other breakers that can be used, the reducing agent utilized canalso be delayed by encapsulating it with a slowly water soluble or othersimilar encapsulating material.

[0039] The gel breaker utilized in a water-containing gelled liquidhydrocarbon fracturing fluid of this invention is generally presenttherein in an amount in the range of from about 0.01% to about 3% byweight of the hydrocarbon liquid, more preferably in an amount in therange of from about 0.05% to about 1%.

[0040] A preferred method of fracturing a subterranean formation inaccordance with the present invention is comprised of the steps of: (a)preparing a gelled liquid hydrocarbon fracturing fluid comprised of ahydrocarbon liquid, a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester, the phosphonic acid ester having the formula:

[0041] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21 or adialkylphosphinic acid having the formula:

[0042] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21; and(b) contacting the subterranean formation with the gelled hydrocarbonfracturing fluid under conditions effective to create at least onefracture in the subterranean formation.

[0043] The ferric iron or aluminum polyvalent metal salt of thephosphonic acid ester or dialkylphosphinic acid is present in thefracturing fluid in an amount in the range of from about 0.1% to about2.5% by weight of the hydrocarbon liquid in the fracturing fluid, morepreferably in an amount in the range of from about 0.2% to about 1%. Theproppant material is present in the fracturing fluid in an amount in therange of from about 1 to about 14 pounds of proppant material per gallonof hydrocarbon liquid in the fracturing fluid. As mentioned, if desired,water may be added to or otherwise contained in the hydrocarbon liquidso that a delayed gel breaker may be utilized. The delayed gel breakermay be present in the fracturing fluid in an amount in the range of fromabout 0.01% to about 3% by weight of the hydrocarbon liquid in thefracturing fluid, more preferably in an amount in the range of fromabout 0.05% to about 1%.

[0044] A preferred method of preparing a gelled liquid hydrocarbon fluidof this invention is comprised of adding a phosphonic acid ester to ahydrocarbon liquid, the phosphonic acid ester having the formula

[0045] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21 or adialkylphosphinic acid having the formula:

[0046] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21, atleast a stoichiometric amount of a polyvalent metal source selected fromferric iron salts and aluminum compounds which reacts with thephosphonic acid ester or dialkylphosphinic acid to form a ferric iron oraluminum polyvalent metal salt thereof, and optionally water and anamount of a delayed gel breaker effective to break the gelledhydrocarbon fracturing fluid.

[0047] The ferric iron or aluminum polyvalent metal salt of thephosphonic acid ester or dialkylphosphinic acid formed in thehydrocarbon liquid is present therein in an amount in the range of fromabout 0.1% to about 2.5% by weight of the hydrocarbon liquid, morepreferably in an amount in the range of from about 0.2% to about 1%. Thedelayed gel breaker, if utilized, is present in the hydrocarbon liquidin an amount in the range of from about 0.01% to about 3% by weight ofthe hydrocarbon liquid, more preferably in an amount in the range offrom about 0.05% to about 1%.

[0048] A preferred hydrocarbon liquid gelling agent of this invention iscomprised of a ferric iron or aluminum polyvalent metal salt of aphosphonic acid ester, the phosphonic acid ester having the formula:

[0049] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21 or adialkylphosphinic acid having the formula:

[0050] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 3 to about 21.

[0051] A more preferred hydrocarbon liquid gelling agent is comprised ofa ferric iron polyvalent metal salt of a phosphonic acid ester, theester having the formula:

[0052] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 9 to about 21 or adialkylphosphinic acid having the formula:

[0053] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H₂₊₁ where n is from about 9 to about 21.

[0054] A preferred gelled liquid hydrocarbon composition of thisinvention is comprised of: a hydrocarbon liquid; a gelling agentcomprising a polyvalent metal salt of a phosphonic acid ester or adialkylphosphinic acid produced from a phosphonic acid ester or adialkylphosphinic acid and a ferric iron salt or an aluminum compound,the phosphonic acid ester having the formula:

[0055] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 9 to about 21 or adialkylphosphinic acid having the formula:

[0056] where R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 9 to about 21.

[0057] As mentioned above, the delayed gel breaker, when present, can bealkaline earth metal oxides including hard burned magnesium oxide,alkali metal carbonates, alkali metal bicarbonates, alkali metalacetates, alkali metal hydroxides, amines and weak acids which areslowly water soluble or are encapsulated with a slowly water soluble orother similar encapsulating material. The delayed gel breaker can alsobe a reducing agent that reduces ferric iron to ferrous ironencapsulated with a slowly water soluble or other similar encapsulatingmaterial. The delayed gel breaker may be present in the gelledhydrocarbon liquid in an amount in the range of from about 0.01% toabout 3% by weight of the hydrocarbon liquid, more preferably in anamount in the range of from about 0.05% to about 1%.

[0058] As will be understood by those skilled in the art, the use of theimproved liquid hydrocarbon gelling agents and gelled liquid hydrocarboncompositions is not limited to fracturing subterranean formations. Forexample, the gelled liquid hydrocarbon compositions can be used forforming gravel packs in well bores, in pipeline pigging operations andin other operations where a gelled hydrocarbon liquid which subsequentlymay be broken into a thin fluid is utilized.

[0059] In order to further illustrate the methods and composition of thepresent invention, the following examples are given.

EXAMPLE 1

[0060] A number of monoesters of alkylphosphonic acids were prepared inthe laboratory as follows: solid dodecylphosphonic acid monomethylester, solid tetradecylphosphonic acid monomethyl ester, solidhexadecylphosphonic acid monomethyl ester, solid octadecylphosphonicacid monomethyl ester, solid C₂₀₋₂₄ phosphonic acid monomethyl ester,solid octadecylphosphonic acid monobutyl ester, liquid octylphosphonicacid monomethyl ester and liquid decylphosphonic acid monomethyl ester.

[0061] The following laboratory procedure was utilized in thepreparation of the above listed esters. Alkylphosphonic acid dimethyl(or dibutyl) esters were first prepared by charging a 250 milliliterthree necked round bottom flask with 0.2 mole of 1-alkene and 0.5 moleof dimethyl or dibutyl phosphite. The flask was fitted with a refluxcondenser, thermometer, temperature controller, septum stopper andnitrogen purge. The mixture was magnetically stirred and heated to 150°C. or the boiling point of the 1-alkene, whichever was lower. 2.5milliliters of t-butyl peroxide was slowly added with a syringe over thecourse of 1 hour. The mixture was heated at 150° C. for another 1.5hours. The excess dialkyl phosphite was removed using vacuumdistillation.

[0062] The following laboratory procedure was utilized in thepreparation of monomethyl (or monobutyl) esters that are liquids at roomtemperature. That is, alkylphosphonic acid monomethyl (or monobutyl)esters were prepared using the alkylphosphonic acid dimethyl (ordibutyl) esters prepared in accordance with the above describedprocedure as follows. 0.045 mole of alkylphosphonic acid dimethyl (ordibutyl) ester was charged to a 100 milliliter round bottom flask. Asolution of 1.9 grams (0.048 mole) of sodium hydroxide in 38 millilitersof methanol was added to the flask and the flask was fitted with areflux condenser. The mixture was stirred magnetically and heated toreflux for 3 hours. 10 milliliters of water and 50 milliliters of hexanewere added and the resulting mixture was shaken. The phases wereseparated and the hexane layer containing the unreacted dimethyl (ordibutyl) ester was discarded. The aqueous layer was washed twice with 20milliliter portions of hexane and the hexane layer was discarded. 3.6milliliters of 38% hydrochloric acid (0.045 mole) was added to theaqueous phase followed by 40 milliliters of water. The mixture wasextracted 3 times with 20 milliliter portions of hexane. The combinedorganic fractions were washed with water and dried over anhydrousmagnesium sulfate. The solvent was removed using a rotary evaporator.The alkylphosphonic acid monomethyl (or monobutyl) esters produced wereliquids at room temperature.

[0063] Alkylphosphonic acid monoesters which are solids at roomtemperature were also prepared. These were the C12 to C24 alkylphosphonic acid mono methyl esters. The following laboratory procedurewas utilized. A 100 milliliters round bottom flask was charged with 0.05mole of alkylphosphonic acid dimethyl ester and the flask was warmed tomelt the solid. A solution of 2.5 g (0.063 mole) of sodium hydroxide in38 milliliters of methanol was added and the flask was fitted with areflux condenser. The mixture was stirred magnetically and heated toreflux for 3 hours. The flask was cooled and 5 milliliters 38%hydrochloric acid (0.062 mole) was added, followed by the addition of125 milliliters of water. The slurry was extracted into hexane. Thehexane solution was washed with water, dried over anhydrous magnesiumsulfate, and concentrated on a rotary evaporator. The product wasallowed to recrystallize, then it was collected on a büchner funnel,washed with hexane, and air dried.

EXAMPLE 2

[0064] A commercially available octylphosphonic acid monomethyl esterwas obtained which contained 55-65% octylphosphonic acid monomethylester, 20-30% octylphosphonic acid and 10-20% octylphosphonic aciddimethyl ester. 2 milliliters of the commercial octylphosphonic acidmonomethyl ester and 2 milliliters of a ferric iron cross-linkercommercially available from Clearwater Inc. of Pittsburgh, Pa. under thetrade designation “HGA-65TM” were added to 200 milliliters of kerosene.Initial cross-linking was observed after 20 seconds of stirring with anoverhead stirrer. A strong cross-linked gel was observed after 1 minute.

[0065] This test shows that the phosphonic acid ester does not have tobe pure, i.e., it can contain portions of the phosphonic acid and thephosphonic acid dialkyl ester.

EXAMPLE 3

[0066] 2 milliliters of the commercially available octylphosphonic acidmonomethyl ester described in Example 2 were added to 200 milliliters ofkerosene along with a ferric iron cross-linker composition. The ferriciron cross-linker composition was comprised of 240 grams of deionizedwater, 60 grams of ferric sulfate pentahydrate and 33.3 grams oftriethanolamine.

[0067] Upon mixing, the cross-linking reaction was slower than thatobserved in Example 2, but good cross-linking was observed after 2 to 3minutes.

EXAMPLE 4

[0068] The commercially available octylphosphonic acid monomethyl esterdescribed in Example 2 was added to No. 2 off-road diesel oil along witha commercially available ferric iron cross-linking composition obtainedfrom Ethox Chemicals, Inc. of Greenville, S.C. sold under the tradedesignation “EA-3™” (see U.S. Pat. No. 6,149,693 issued to Geib on Nov.21, 2000). Three different mixtures were prepared having the quantitiesof components shown in Table I below. After mixing, each of the mixtureswas placed in a Model 50 viscometer at 68° C. and the viscosities of themixtures were observed over time. The results of these tests are givenin Table I below. TABLE I Viscosities Of Gelled Diesel Oil UsingCommercially Available Gelling Agent Components At 68° C. Time,Viscosity, cp. @ 170/sec minutes Mixture A¹ Mixture B² Mixture C³ 30 297169 197 60 243 172 210 90 218 187 212 120 205 209 204 150 193 217 199180 184 218 193 210 175 218 188 240 167 217 184 270 158 216 182 300 152217 —

[0069] From Table I it can be seen that the commercially availableoctylphosphonic acid monomethyl ester and cross-linker produced rapidcross-linking and excellent viscosities.

EXAMPLE 5

[0070] The procedure of Example 4 was repeated except that theoctylphosphonic acid monomethyl ester was synthesized in accordance withthe procedure set forth in Example 1 and the third mixture tested, i.e.,mixture F, included magnesium oxide breaker. The results of these testsare given in Table II below. TABLE II Viscosities Of Gelled Diesel OilUsing Synthesized Octylphosphonic Acid Monomethyl Ester And CommercialFerric Iron Cross-Linking Composition At 68° C. Time, Viscosity, cp. @170/sec minutes Mixture D¹ Mixture E² Mixture F³ 4 299 388 395 30 131143 85 60 135 146 47 90 140 151 34 120 146 156 25 150 149 160 17 180 —162 10 210 — 163 — 240 — 164 —

[0071] From Table II it can be seen that the synthesized octylphosphonicacid monomethyl ester produced excellent gels. In addition, mixture Fincluding magnesium oxide gel breaker showed an increased viscosity as aresult of neutralization of the phosphonic acid ester by the magnesiumoxide breaker therein after which the gel was broken.

EXAMPLE 6

[0072] The procedure of Example 4 was repeated except that thephosphonic acid ester used was synthesized hexadecylphosphonic acidmonomethyl ester. The results of these tests are given in Table III setforth below. TABLE III Viscosities Of Gelled Diesel Oil UsingSynthesized Hexadecylphosphonic Acid Monomethyl Ester And CommercialFerric Iron Cross-Linking Composition At 68° C. Time, Viscosity, cp. @170/sec minutes Mixture G¹ Mixture H² Mixture I³ Mixture J⁴ Mixture K⁵Mixture L⁶ Mixture M⁷ Mixture N⁸ 3.5 36 121 70 162 107 179 235 292 30145 199 190 183 165 177 175 186 60 171 176 169 195 166 187 172 181 90177 186 169 208 167 192 173 177 120 187 197 175 213 169 194 174 172 150189 203 179 218 175 200 178 176 180 191 209 189 221 181 202 178 174 195193 209 190 222 181 203 181 174

[0073] From Table III it can be seen that synthesizedhexadecylphosphonic acid monomethyl ester and the ferric ironcross-linker utilized form excellent gels in diesel oil at 68° C.

EXAMPLE 7

[0074] The test procedure of Example 4 was repeated except thatsynthesized octadecylphosphonic acid monomethyl ester was utilized, thetemperature of the gelled diesel oil was increased over time and two ofthe four gelled mixtures tested contained a magnesium oxide breaker. Theresults of these tests are given in Table IV below. TABLE IV ViscositiesOf Gelled Diesel Oil Using Synthesized Octadecylphosphonic AcidMonomethyl Ester And Commercial Ferric Iron Cross-Linking Composition AtVarious Temperatures Mixture O¹ Mixture P² Mixture Q³ Mixture R⁴ Time,Temp., Viscosity, cp. Temp., Viscosity, cp. Temp., Viscosity, cp. Temp.,Viscosity, cp. minutes ° C. @ 170/sec ° C. @ 170/sec ° C. @ 170/sec ° C.@ 170/sec 0 33 236 32 165 26 210 27 260 30 66 243 66 200 67 245 55 29560 67 247 68 220 68 250 88 320 90 67 247 68 222 68 253 117 355 120 67247 68 227 68 255 141 375 150 86 254 85 265 86 280 145 390 180 132 44129 60 131 45 152 310 210 145 37 145 42 145 35 162 150 240 146 36 146 42146 32 173 27 270 — — — — — — 174 16 300 — — — — — — 183 15 330 — — — —— — 193 14

[0075] As can be seen from Table IV, synthesized octadecylphosphonicacid monomethyl ester and the ferric iron cross-linker utilized formexcellent gels in diesel oil over a broad temperature range. Further,the magnesium oxide breaker neutralized the acid ester which increasedthe viscosity attained over a broad range of temperatures.

EXAMPLE 8

[0076] The test procedure of Example 4 was repeated except that a TempcoRheo-15 rheometer was utilized to measure apparent viscosities atvarious temperatures with fluids containing 40% CO₂ by volume. One ofthe test mixtures was formed with a #2 Off Road Diesel hydrocarbon fluidand another test mixture included magnesium oxide. The results of thesetests are set forth in Table V below. TABLE V Viscosities Of GelledDiesel Using Commercially Available Gelling Agent Components And 40%Carbon Dioxide By Volume At Various Temperatures Mixture S¹ Mixture T²Mixture U³ Time, Temp., Viscosity, cp. Temp., Viscosity, cp. Temp.,Viscosity, cp. minutes ° C. @ 170/sec ° C. @ 170/sec ° C. @ 170/sec 0 10120 7 120 7 100 10 66 155 52 195 60 295 20 85 115 66 205 63 330 30 85 9568 195 66 340 40 85 85 71 190 68 345 50 85 85 74 175 71 350 60 85 85 77165 72 350 70 — — 82 145 74 340 80 — — 85 130 77 335 90 — — 88 110 79320 100 — — 91 90 85 315 110 — — 93 80 88 300 120 — — 96 65 90 285 130 —— 99 45 91 265 140 — — 102 35 93 240 150 — — 104 20 96 210 # and 0.240grams of magnesium oxide breaker per liter of diesel oil containing 40%by volume carbon dioxide.

[0077] From Table V it can be seen that excellent gels were formed eventhough the gels contained 40% by volume carbon dioxide. Also, asignificant increase in viscosity was realized when the gel includedonly enough magnesium oxide breaker to partially neutralize the octylphosphonic acid monomethyl ester.

EXAMPLE 9

[0078] Various synthesized phosphonic acid esters were added in variousamounts to diesel oil or kerosene along with various amounts of ETHOX“EA-3™” ferric iron cross-linker compositions and the resulting gelswere observed. The results of these tests are set forth in Table VIbelow. TABLE VI Observations Of Various Gels Formed With AlkylphosphonicAcid Monomethyl Esters And Commercial Cross-Linkers Ester Cross-LinkerHydrocarbon Amount In Amount, ml/L of Liquid Hydrocarbon hydrocarbonUsed Ester Liquid Cross-Linker liquid Observations Off-road DieselOctylphosphonic acid  2.0 ml/L Ethox “EA-3 ™” 2 weak elastic gelmonomethyl ester Off-road Diesel Octylphosphonic acid 33.0 ml/L Ethox“EA-3 ™” 3 weak lipping gel monomethyl ester Off-road DieselOctylphosphonic acid  5.0 ml/L Ethox “EA-3 ™” 5 strong lipping gelmonomethyl ester Off-road Diesel Decylphosphonic acid  5.0 ml/L Ethox“EA-3 ™” 10 weak elastic gel monomethyl ester Off-road DieselDecylphosphonic acid 10.0 ml/L Ethox “EA-3 ™” 5 lipping gel monomethylester Kerosene Hexadecylphosphonic  9.9 g/L Ethox “EA-3 ™” 10 verystrong lipping acid monomethyl ester gel Kerosene Octadecylphosphonic 8.0 g/L Ethox “EA-3 ™” 6 very strong lipping acid monobutyl ester gelKerosene Octylphosphonic acid 10.0 ml/L Aluminum compound² 0.8 goodlipping gel monomethyl ester¹

EXAMPLE 10

[0079] The procedure described in Example 4 was repeated except thatmagnesium oxide breaker was included in the three mixtures that weretested. In addition, one of the gels was produced utilizing ahydrocarbon liquid commercially available from Trisol Corp. of Sundre,Alberta, Canada under the trade name “FRACSOL™” to which was added 40%by total volume carbon dioxide. The results of the tests are given inVII below. TABLE VII Break Times Of Various Gels With Magnesium OxideMixture V¹ Mixture W² Mixture X³ Time, Temp., Viscosity, cp. Temp.,Viscosity, cp. Temp., Viscosity, cp. minutes ° C. @ 170/sec ° C. @170/sec ° C. @170/sec 5 31 366 33 375 39 370 10 46 365 48 307 68 365 1554 365 55 240 85 360 20 59 364 58 173 85 200 25 62 363 61 105 85 70 3064 360 62 83 85 30 35 65 357 64 76 85 15 40 66 353 65 67 85 13 45 67 33565 62 85 10 50 67 318 66 56 85 9 55 67 302 66 51 85 5 60 68 293 66 47 852 90 68 185 66 34 120 68 97 67 25 150 68 74 67 17 180 68 67 67 11 210 6860 240 68 54 270 68 47 300 68 35 330 68 25 360 68 18 390 68 14 420 68 12# liter of “FRACSOL  ™” hydrocarbon liquid mixed with 40% by volumecarbon dioxide. Mixture X also contained water.

[0080] From Table VII, it can be seen that complete progressive breakswere obtained by the presence of the magnesium oxide. The synthesizedphosphonic acid ester required significantly less breaker and stillshowed a faster break rate than the commercial phosphonic acid ester.The gel containing 60% by volume “FRACSOL™” hydrocarbon liquid and 40%by volume carbon dioxide also achieved a progressive and complete breakas a result of the presence of the magnesium oxide.

EXAMPLE 11

[0081] Gelled hydrocarbon liquid test samples were prepared by combining0.02M (6.4 g/L) of hexadecylphosphonic acid monomethyl ester and 5milliliters of ethox “EA-3™” ferric iron cross-linker composition to 1liter of off-road diesel oil. Various reducing agents for reducingferric iron to ferrous iron and thereby breaking the gels were added tothe test samples. Thereafter, the viscosities of the test samples overtime were measured to determine the effectiveness of the reducing agentsin breaking the gels. The results of these tests are given in Table VIIIbelow. TABLE VIII Break Times Of Diesel Oil Gel¹ Containing VariousReducing Agents @ 90° C. Reducing Viscosity, cp. @ 170/sec At Time AgentUsed 0 2 hrs. 21 hrs. 45 hrs. 242 hrs. Blank - No 60 66 66 66 66Reducing Agent Stannous 7 3 — — — Chloride dihydrate Thioglycolic Acid45 3 — — — Sodium 141 18 3 — — Diethyldithiocarbamate Sodium 123 42 30 3— Dimethyldithiocarbamate Hydrazine Sulfate 45 96 57 33 3 Hydroxylamine75 69 15 3 — Hydrochloride # diethyldithiocarbamate = 22.53 g/L; 0.1 Mfor sodium dimethyldithiocarbamate The off-road diesel oil gelscontained water.

[0082] From Table VIII it can be seen that reducing agents comprised ofstannous chloride, thioglycolic acid, sodium diethyldithiocarbamate,sodium dimethyldithiocarbamate and hydrazine sulfate can be utilized asefficient reducing agent breakers for the hydrocarbon gels of thisinvention, at 90° C.

[0083] Additional reducing agents were evaluated but found to be tooweak with phosphonates gels, at 90° C. However, it is understood theadditional reducing agents could be the preferred reducing agents athigher temperatures where a slower rate of reaction is required. Theadditional reducing agents include, but are not limited to, sodiumhypophosphite, potassium iodide, 2-mercaptoethanol (thioglycol),ascorbic acid, sodium thiosulfate, sodium dithionite, sodium sulfite andsalts thereof.

EXAMPLE 12

[0084] Various alkylphosphonic acid monomethyl esters were dissolved ina high boiling point mineral oil in amounts such that 0.01 M solutionswere formed. The solutions were each distilled in accordance with ASTMD-86 and the distillates obtained were analyzed for phosphorus byInductively Coupled Plasma methodology (ASTM D-4951). The results ofthese tests are given in Table IX. TABLE IX Volatile Phosphorus FormedFrom Distillation Of Alkylphosphonic Acid Monomethyl Esters In MineralOil Phosphorus in Ester Distillate, ppm octylphosphonic acid monomethylester 148 decylphosphonic acid monomethyl ester 38 dodecylphosphonicacid monomethyl ester 12 tetradecylphosphonic acid monomethyl ester 6hexadecylphosphonic acid monomethyl ester 5 octadecylphosphonic acidmonomethyl ester 3 C₂₀₋₂₄ alkanephosphonic acid monomethyl ester <1

[0085] Table 1X shows a clear trend in which the volatile phosphorusproduced by the alkyl-phosphonic acid monomethyl esters is a function ofmolecular weight. Tetradecylphosphonic acid monomethyl ester shows a 96%reduction in volatile phosphorus over the octylphosphonic acidmonomethyl ester. The fact that the C₂₀₋₂₄ alkylphosphonic acidmonomethyl ester had no detectable volatile phosphorus shows thatdecomposition due to hydrolysis has been eliminated under the testconditions.

[0086] From Table IX it is apparent the alkylphosphonic acid monomethylesters of C14 (tetradecyl) or higher are preferred to minimize volatilephosphorus. Of these, tetradecylphosphonic acid monomethyl ester is mostpreferred to reduce volatile phosphorus while retaining good solubilityproperties at room temperature. Additionally, mild alkyl group branchingis desirable to maintain liquid properties of the mono methyl ester.

[0087] Thus, the present invention is well adapted to carry out theobjects and attain the benefits and advantages mentioned as well asthose which are inherent therein. While numerous changes to the methodsand compositions can be made by those skilled in the art, such changesare encompassed within the spirit of this invention as defined by theappended claims.

What is claimed is:
 1. A method of treating a subterranean formationcomprising the steps of: (a) preparing a gelled liquid hydrocarbon fluidcomprising a hydrocarbon liquid, a ferric iron or aluminum polyvalentmetal salt of a dialkylphosphinic acid, said dialkylphosphinic acidhaving the formula:

wherein R¹ is an alkyl group having from 1 to 4 carbon atoms and R² isan alkyl or phenyl group having from 6 to 24 carbon atoms; and (b)contacting said subterranean formation with said gelled hydrocarbonfluid under conditions effective to treat said subterranean formation.2. The method of claim 1 wherein said hydrocarbon liquid is selectedfrom the group consisting of olefins, kerosene, diesel oil, gas oil,fuel oil, petroleum distillate and crude oil.
 3. The method of claim 1wherein said polyvalent metal salt of a dialkylphosphinic acid isproduced by reacting said dialkylphosphinic acid with a ferric ironcompound.
 4. The method of claim 1 wherein said polyvalent metal salt ofa dialkylphosphinic acid is produced by reacting said dialkylphosphinicacid with an aluminum compound.
 5. The method of claim 1 wherein saidferric iron or aluminum polyvalent metal salt of a dialkylphosphinicacid is present in said hydrocarbon liquid in an amount in the range offrom about 0.1% to about 2.5% by weight of said hydrocarbon liquid. 6.The method of claim 1 wherein said gelled liquid hydrocarbon fluid isdefined further to include an effective amount of a delayed gel breakerwhich is selected from the group consisting of magnesium oxide, alkalimetal carbonates, alkali metal bicarbonates, alkali metal acetates,alkali metal hydroxides, amines and weak acids which are slowly watersoluble or are encapsulated with a slowly water soluble encapsulatingmaterial.
 7. The method of claim 6 wherein said delayed gel breaker isslowly water soluble hard burned magnesium oxide.
 8. The method of claim1 wherein said gelled liquid hydrocarbon fluid is defined further toinclude an effective amount of a delayed gel breaker which is a reducingagent that reduces ferric iron to ferrous iron.
 9. The method of claim 8wherein said reducing agent is selected from the group consisting ofstannous chloride, thioglycolic acid and its salts, hydrazine sulfate,sodium diethyldithiocarbamate, sodium dimethyldithiocarbamate, sodiumhypophosphite, hydroxylamine hydrochloride, thioglycol, ascorbic acidand its salts, sodium thiosulfate, and sodium sulfite.
 10. The method ofclaim 6 wherein said gel breaker is present in said gelled hydrocarbonliquid in an amount in the range of from about 0.01% to about 3% byweight of said hydrocarbon liquid.
 11. A method of preparing a gelledliquid hydrocarbon fluid comprising adding a dialkylphosphinic acid to ahydrocarbon liquid, the dialkylphosphinic acid having the formula:

wherein R¹ is an alkyl group having from 1 to 4 carbon atoms and R² isan alkyl or phenyl group having from 6 to 24 carbon atoms, and at leasta stoichiometric amount of a polyvalent metal source selected fromferric iron salts and aluminum compounds which react with saiddialkylphosphinic acid to form a ferric iron or aluminum polyvalentmetal salt thereof which gels said hydrocarbon liquid.
 12. The method ofclaim 11 wherein said hydrocarbon liquid is selected from the groupconsisting of olefins, kerosene, diesel oil, gas oil, fuel oil,petroleum distillate, and crude oil.
 13. The method of claim 11 whereinsaid ferric iron or aluminum polyvalent metal salt of saiddialkylphosphinic acid formed in said hydrocarbon liquid is presenttherein in an amount in the range of from about 0.1% to about 2.5% byweight of said hydrocarbon liquid.
 14. The method of claim 11 definedfurther to include adding a delayed gel breaker to said hydrocarbonliquid which is selected from the group consisting of magnesium oxide,alkali metal carbonates, alkali metal bicarbonates, alkali metalacetates, alkali metal hydroxides, amines and weak acids which areslowly water soluble or are encapsulated with a slowly water solubleencapsulating material.
 15. The method of claim 14 wherein said delayedgel breaker is slowly water soluble hard burned magnesium oxide.
 16. Themethod of claim 11 defined further to use ferric iron salts and the stepof adding a delayed gel breaker to said hydrocarbon liquid which is areducing agent that can subsequently reduce ferric iron to ferrous iron.17. The method of claim 16 wherein said reducing agent is selected fromthe group consisting of stannous chloride, thioglycolic acid and itssalts, hydrazine sulfate, sodium diethyldithiocarbamate, sodiumdimethyldithiocarbamate, sodium hypophosphite, hydroxylaminehydrochloride, thioglycol, ascorbic acid and its salts, sodiumthiosulfate and sodium sulfite.
 18. The method of claim 14 wherein saidgel breaker is present in said gelled hydrocarbon liquid in an amount inthe range of from about 0.01% to about 3% by weight of said hydrocarbonliquid.
 19. A gelled liquid hydrocarbon fluid composition comprising: ahydrocarbon liquid; a gelling agent comprising a polyvalent metal saltof a phosphonic acid ester produced from a phosphonic acid ester and aferric iron salt or an aluminum compound or a polyvalent metal salt of adialkylphosphinic acid produced from a dialkylphosphinic acid and aferric iron salt or an aluminum compound, said phosphonic acid esterhaving the formula:

where R represents a linear or branched alkyl chain having the generalformula C_(n)H_(2n+1) where n is from 3 to 21 or a dialkylphosphinicacid having the formula:

where R represents a linear or branched alkyl chain having the generalformula C_(n)H₂₊₁ where n is from 3 to 21; and a delayed gel breakerpresent in an amount effective to break the gel formed by said gellingagent and said hydrocarbon liquid.
 20. The composition of claim 19wherein n is from 9 to
 21. 21. The composition of claim 19 wherein saidhydrocarbon liquid is selected from the group consisting of olefins,kerosene, diesel oil, gas oil, fuel oil, petroleum distillate, and crudeoil.
 22. The composition of claim 19 wherein said ferric iron salt isselected from the group consisting of ferric sulfate and ferricchloride.
 23. The composition of claim 19 wherein said aluminum compoundis selected from the group consisting of aluminum chloride, aluminumsulfate and aluminum isopropoxide.
 24. The composition of claim 19wherein said delayed gel breaker is selected from the group consistingof magnesium oxide, alkali metal carbonates, alkali metal bicarbonates,alkali metal acetates, alkali metal hydroxides, amines and weak acidswhich are slowly water soluble or are encapsulated with a slowly watersoluble encapsulating material.
 25. The composition of claim 19 whereinsaid delayed gel breaker is slowly water soluble, hard burned magnesiumoxide.
 26. The composition of claim 19 wherein said delayed gel breakeris a reducing agent that reduces ferric iron to ferrous ironencapsulated with a slowly water soluble encapsulating material.
 27. Thecomposition of claim 26 wherein said reducing agent is selected from thegroup consisting of stannous chloride, thioglycolic acid and its salts,hydrazine sulfate, sodium diethyldithiocarbamate, sodiumdimethyldithiocarbamate, sodium hypophosphite, hydroxylaminehydrochloride, thioglycol, ascorbic acid and its salts, sodiumthiosulfate, and sodium sulfite.
 28. The composition of claim 27 whereinsaid gel breaker is present in said gelled hydrocarbon liquid in anamount in the range of from about 0.01% to about 3% by weight of saidhydrocarbon liquid.
 29. A gelled hydrocarbon liquid compositioncomprising: a liquid hydrocarbon; and an effective amount of a gellingagent to gel the composition comprising a polyvalent metal salt of adialkylphosphinic acid produced from a dialkylphosphinic acid and aferric iron salt or an aluminum compound, said phosphinic acid havingthe formula:

wherein R¹ is an alkyl group having from 1 to 4 carbon atoms and R² isan alkyl or phenyl group having from 6 to 24 carbon atoms.
 30. Thecomposition of claim 29 wherein said hydrocarbon liquid is selected fromthe group consisting of olefins, kerosene, diesel oil, gas oil, fueloil, petroleum distillate and crude oil.
 31. The composition of claim 29wherein said polyvalent metal salt of a dialkylphosphinic acid isproduced by reacting said dialkylphosphinic acid with a ferric ironcompound.
 32. The composition of claim 29 wherein said polyvalent metalsalt of a dialkylphosphinic acid is produced by reacting saiddialkylphosphinic acid with an aluminum compound.
 33. The composition ofclaim 1 wherein said ferric iron or aluminum polyvalent metal salt of adialkylphosphinic acid is present with said hydrocarbon liquid in anamount in the range of from about 0.1% to about 2.5% by weight of saidhydrocarbon liquid.
 34. A gelled hydrocarbon liquid compositioncomprising: a hydrocarbon liquid and a dialkylphosphinic acid having theformula:

wherein R¹ is an alkyl group having from 1 to 4 carbon atoms and R² isan alkyl or phenyl group having from 6 to 24 carbon atoms.
 35. Thecomposition of claim 34 wherein said hydrocarbon liquid is selected fromthe group consisting of olefins, kerosene, diesel oil, gas oil, fueloil, petroleum distillate and crude oil.
 36. The composition of claim 34wherein said dialkylphosphinic acid has the formula:

wherein R represents a linear or branched alkyl chain having the generalformula C_(n)H₂₊₁ where n is from 3 to
 21. 37. The composition of claim36 wherein R represents a linear or branched alkyl chain having thegeneral formula C_(n)H_(2n+1) where n is from about 9 to about
 21. 38. Amethod of treating a subterranean formation comprising the steps of:preparing a gelled hydrocarbon fluid comprising a hydrocarbon liquid anda dialkylphosphinic acid having the formula:

wherein R¹ is an alkyl group having from 1 to 4 carbon atoms and R² isan alkyl or phenyl group having from 6 to 24 carbon atoms; and placingthe gelled fluid in a subterranean formation.
 39. The composition ofclaim 38 wherein said hydrocarbon liquid is selected from the groupconsisting of olefins, kerosene, diesel oil, gas oil, fuel oil,petroleum distillate and crude oil.
 40. The composition of claim 38wherein said dialkylphosphinic acid has the formula:

wherein R represents a linear or branched alkyl chain having the generalformula C_(n)H_(2n+1) where n is from 3 to
 21. 41. The composition ofclaim 38 wherein R represents a linear or branched alkyl chain havingthe general formula C_(n)H_(2n+t) where n is from about 9 to about 21.